US4151342A - Process for producing fluoroelastomer and crosslinked polymer thereof - Google Patents

Process for producing fluoroelastomer and crosslinked polymer thereof Download PDF

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US4151342A
US4151342A US05/860,198 US86019877A US4151342A US 4151342 A US4151342 A US 4151342A US 86019877 A US86019877 A US 86019877A US 4151342 A US4151342 A US 4151342A
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fluoroelastomer
vulcanization
mole
tetrafluoroethylene
polymerization
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Tetsuya Uchino
Michio Hisasue
Hiroaki Kojima
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AGC Inc
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Asahi Glass Co Ltd
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
    • C08F214/18—Monomers containing fluorine
    • C08F214/26—Tetrafluoroethene
    • C08F214/265—Tetrafluoroethene with non-fluorinated comonomers
    • C08F214/267—Tetrafluoroethene with non-fluorinated comonomers with non-fluorinated vinyl ethers
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/31504—Composite [nonstructural laminate]
    • Y10T428/31855—Of addition polymer from unsaturated monomers

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  • the present invention relates to a process for producing a fluoroelastomer, more particularly, it relates to a process for producing a novel fluoroelastomer of propylene-tetrafluoroethylene-glycidyl vinyl ether terpolymer.
  • the fluoroelastomers of propylene-tetrafluoroethylene copolymer have excellent heat resistance and chemical resistance whereas they have inferior vulcanization properties.
  • a novel fluoroelastomer which is vulcanizable and comprises 50 to 65 mole % of tetrafluoroethylene component, 35 to 50 mole % of propylene component and 0.01 to 10 mole % of glycidyl vinyl ether component was obtained. It is especially preferable to produce a fluoroelastomer comprising 53 to 60 mole % of tetrafluoroethylene component, 40 to 47 mole % of propylene component, and 0.2 to 5 mole % of glycidyl vinyl ether component.
  • the content of the glycidyl vinyl ether is too small, the improvement of the vulcanization properties is not enough whereas when it is too much, the heat resistance in aging is deteriorated and the cost of the raw materials is disadvantageously high.
  • the contents of tetrafluoroethylene and propylene are preferably selected from the above-mentioned range from the viewpoints of heat resistance, chemical resistance and easy availability.
  • the terpolymerization of the present invention can be a bulk polymerization, a suspension polymerization, an emulsion polymerization, and a solution polymerization.
  • a conventional catalytic polymerization, a modified redox polymerization, and a high energy ionizing radiation polymerization can be adopted.
  • tetrafluoroethylene tetrafluoroethylene
  • propylene and glycidyl vinyl ether it is possible to add suitable other monomer such as ethylene, isobutylene, vinyl fluoride, vinylidene fluoride, hexafluoropropylene, fluorovinyl ether, alkyl vinyl ether, chlorotrifluoroethylene etc.
  • suitable other monomer such as ethylene, isobutylene, vinyl fluoride, vinylidene fluoride, hexafluoropropylene, fluorovinyl ether, alkyl vinyl ether, chlorotrifluoroethylene etc.
  • the content of the other monomer component is usually less than 15 mole %.
  • the molecular weight of the fluoroelastomer is preferably more than about 30,000 from the viewpoint of characteristics of the vulcanized product such as tensile strength.
  • the molecular weight of the copolymer should not be too high from the viewpoints of both of the processability and the characteristics of the vulcanized product. It is optimum to produce the fluoroelastomer having a molecular weight of about 50,000 to 150,000.
  • the process of the present invention is carried out under various polymerization systems and polymerization conditions. It is possible to carry out the copolymerization in an organic solvent such as fluoro- or fluorochloro-saturated hydrocarbons e.g. trichloromonofluoromethane, trichlorotrifluoroethane and perfluorocyclobutane (Freon® type solvents) and alcohols e.g. tertiary butanol. When the organic solvent is used, the copolymerization can be carried out at -40° C. to +150° C. under relatively low reaction pressure such as about 1 to 50 Kg/cm 2 .
  • an organic solvent such as fluoro- or fluorochloro-saturated hydrocarbons e.g. trichloromonofluoromethane, trichlorotrifluoroethane and perfluorocyclobutane (Freon® type solvents) and alcohols e.g. ter
  • a perfluoroalkyl or perfluorochloroalkyl type dispersing agent is preferably used.
  • a dispersion stabilizer such as chlorinated hydrocarbons, liquid hydrocarbons, trichlorotrifluoroethane and tertiary butanol, a reaction accelerator and other additives.
  • Polymerization initiators such as peroxides, azo compounds and persulfates can be used.
  • the copolymerization can be also carried out by a high energy ionizing radiation such as ⁇ -ray resulted by cobalt-60.
  • the copolymerization in an aqueous medium it is possible to carry it out at about 50° to 100° C. under a pressure of about 5 to 200 Kg/cm 2 .
  • a redox catalyst used as a polymerization initiator, the copolymerization can be carried out at lower temperature such as -20° C. to +50° C.
  • the process of the present invention can be carried out by a batch system, a semi-continuous system or a continuous system.
  • the polymerization conditions, polymerization operation and polymerization apparatus can be preferably selected depending upon the purpose and the polymerization system.
  • a transparent or white fluoroelastomer having rubber-like elasticity can be obtained.
  • the fluoroelastomer having superior vulcanizability than that of the conventional propylene-tetrafluoroethylene copolymer (elastomer) can be obtained.
  • the resulting fluoroelastomer can be treated by various crosslinking agents such as organic peroxides and amines to crosslink it whereby a rubber like crosslinked product is obtained. It is possible to crosslink by high energy ionizing radiation such as ⁇ -rays or electron rays. In this case, it is possible to add various crosslinking adjuvants, fillers and reinforcing agents to give various compositions for vulcanization.
  • various crosslinking agents such as organic peroxides and amines to crosslink it whereby a rubber like crosslinked product is obtained. It is possible to crosslink by high energy ionizing radiation such as ⁇ -rays or electron rays. In this case, it is possible to add various crosslinking adjuvants, fillers and reinforcing agents to give various compositions for vulcanization.
  • novel fluoroelastomers of the present invention an be vulcanized in various formulations under various conditions. It is especially characteristic to be vulcanizable at low temperature such as room temperature by selecting a specific formulation. Thus, the fluoroelastomers of the present invention can be also utilized as the room temperature vulcanizable elastomer.
  • tertiary amines e.g. monoamines, polyamines or salts thereof or a mixture of the tertiary amine and a hydroxyl compound having at least one --OH group
  • a vulcanizing agent it is possible to vulcanize the elastomer at room temperature whereby the vulcanizing velocity is sufficiently high and vulcanized products having excellent heat stability can be obtained.
  • Suitable tertiary amines include benzyl dimethyl amine, ⁇ -methylbenzyl dimethyl amine, dimethyl aminomethyl phenol, tris (dimethyl aminomethyl) phenol, diethylaminopropyl amine, N-aminoethyl piperadine, ethyl methyl imidazole, triethylene diamine, N,N'-bis(alkyl) piperadine, 4,4'-trimethylenedipyridine, 2,3-bis(2-pyridyl)-5,6-dihydropyradine, N-ethyl morphorine, 1,8-diaza bicyclo(5,4,0) undecene-7 and salts thereof.
  • Suitable hydroxyl compounds used with the tertiary amine include octanol, cyclohexanol, phenol, ethyleneglycol, propyleneglycol, polyethyleneglycol, polypropyleneglycol, hydroquinone, catechol, resorcinol, 2,2'-bis(4-hydroxyphenyl) propane[bisphenol A], 1,3,5-trihydroxybenzene, dihydroxynaphthalene, 4,4'-dihydroxydiphenyl, 4,4'-dihydroxystilbene, 2,2'-bis(4-hydroxyphenyl) butane [bisphenol B], 2,4-dihydroxybenzophenone, 2,4-dihydroxybenzoate, 4,4'-dihydroxydiphenylsulfone, 2-methyl resorcinol, trimethylol allyloxyphenol and tris(4-hydroxyphenyl) methane.
  • vulcanizing agents such as aromatic polyamines can be also used though chemical stability of crosslinkage is slightly inferior.
  • Suitable aromatic polyamines include xylene diamine, methaphenylene diamine, diamino-diphenyl methane and diaminodiphenyl sulfone.
  • alicyclic or heterocyclic polyamines such as menthane diamine and bisaminopropyl tetraoxa-spiroundecene.
  • the typical formulations for vulcanization at room temperature are as follows.
  • a vulcanized elastomer having enough strength such as tensile strength of higher than 100 Kg/cm 2 . It is possible to improve the heat resistance by incorporating a metal oxide or silica.
  • a solution paint by dissolving the composition in a suitable solvent.
  • a vulcanized rubber coat having high strength can be obtained by coating the solution paint and maintaining it for 3 to 14 days after the coating.
  • Suitable solvents include ethyl acetate, tetrahydrofuran, and 1,1,2-trichlorotrifluoroethane.
  • additives used in the conventional crosslinking processes can be also added in the crosslinking process of the fluoroelastomer of the present invention.
  • additives include metal oxides such as magnesium oxide and lead oxide; reinforcing agents such as carbon black and fine silica; other fillers; pigments; antioxidants and stabilizers.
  • the additive When the additive is added to the fluoroelastomer, it is preferable to uniformly mix it with the fluoroelastomer.
  • the mixing operation is usually carried out by using the conventional rubber blending roll mill and Bumbary mixer, the condition for the mixing operation is not critical.
  • the additives can be thoroughly dispersed in the fluoroelastomer. It is preferable to select the optimum condition and operation in the mixing operation depending upon the kinds of the raw materials and the ratios thereof and the purposes.
  • the fluoroelastomer obtained by the process of the present invention can be vulcanized at the conventional high temperature of 100° to 250° C. as well as at room temperature.
  • the above-mentioned vulcanizing agents and adjuvants can be used.
  • the heat crosslinking process using the chemical crosslinking agent can be the conventional process.
  • the mixture is heated in a mold by means of a conventional press, transfer and injection molding, or the mixture is fabricated by the extrusion process followed by heating in an air or steam oven or other device. It is preferable to select the optimum condition in the heat crosslinking process depending upon the kinds of the raw materials and the ratios thereof.
  • the temperature in the crosslinking process is usually in a range of about 80° to 250° C. preferably about 120° to 200° C.
  • the time for heating is not critical and it is usually in a range of 1 minute to 2 hours preferably 3 minutes to 2 hours depending upon the kind of the chemical crosslinking agent. When the temperature is high, the time for heating can be short.
  • the crosslinked copolymer can be post cured improve its physical properties. For example, the post cure treatment is carried out at 150° to 250° C. preferably 180° to 230° C. for about 15 to 25 hours.
  • the crosslinked fluoroelastomers produced by the process of the present invention have high heat resistance and chemical resistance as well as high solvent resistance except for certain solvents of such as lower alkane, ketones and esters. Accordingly, the crosslinked fluoroelastomers can be effectively used for various usages requiring elasticity in various conditions for the uses, for example, O-ring for cars, gaskets, valve-stem seals, diaphragms, sealings for dry-cleaning apparatus, pipe, flexible joints, hoses for chemical industrial uses, rolls, packings and grooves.
  • the crosslinked fluoroelastomers are especially useful as the materials which contact with an oil, a solvent or a corrosive liquid.
  • the crosslinked fluoroelastomers can be molded in a form of pipe or rod and they can be also processed as a primary step to form a film or a tape which is further processed by a lamination, a coating and a wind-wrapping as the secondary step.
  • the autoclave was purged with nitrogen, 0.9 g (0.009 mole) of glycidyl vinyl ether(GVE) 5.6 g (0.13 mole) of propylene (P) and 80 g (0.8 mole) of tetrafluoroethylene (4F) were charged under spontaneous pressure.
  • GVE glycidyl vinyl ether
  • P propylene
  • F tetrafluoroethylene
  • the mixture was stirred at 300 rpm and the temperature in the autoclave was raised to 35° C.
  • the monomer mixed gas of 4F, P and GVG of molar ratios of 53:45:2 was charged to maintain the pressure of 26 Kg/cm 2 for 8 hours.
  • the remained monomers were purged and the resulting latex was discharged and 1% aqueous solution of CaCl 2 added to coagulate and the product was washed and dried to obtain 81.0 g of a polymer.
  • the resulting polymer had molar ratios of 54.1:43.8:2.1 of tetrafluoroethylene(4F) component, propylene(P) component and glycidyl vinyl ether(GVE) component (NMR analysis), and had about 30% hydrated glycidyl groups (IR analysis).
  • the copolymer had an average number molecular weight of 75,000 and mooney viscosity (ML 1+4 ) at 100° C. of 68 and a Shore A hardness of 45.
  • a vulcanization was carried out by admixing 100 wt.parts of a copolymer with 1 wt.part of hydroquinone, 0.5 wt.part of tris(dimethylaminomethyl) phenol, 25 wt.parts of MT carbon and 10 wt.parts of lead oxide and press-vulcanizing the mixture at 150° C. under the pressure of 100 Kg/cm 2 for 20 minutes.
  • the product was taken out from the mold and was heated at 200° C. for 22 hours in an oven to vulcanize it.
  • the main mechanical properties of the vulcanized product and the test result of heat aging test are shown in Table 1.
  • Example 1 In accordance with the process of Example 1 except charging 0.45 g(0.0045 mole) of glycidyl vinyl ether at the initiation and charging the monomer mixed gas of 4F, P and GVE of molar ratios of 51:45:1, during the reaction.
  • the copolymerization was carried out for 6 hours to obtain 69.8 g of the polymer having molar ratios of 53.1:45.8:1.1 of 4F component, P component and GVE component and an average number molecular weight of 69,000, and mooney viscosity (ML 1+4 ) at 100° C. of 77.
  • Example 1 In accordance with the process of Example 1, the vulcanization of the resulting polymer was carried out and the physical properties of the vulcanized product were tested. The results are shown in Table 1.
  • Example 1 In accordance with the process of Example 1 except using 2 wt.parts of diaminodiphenyl methane instead of hydroquinone and tris(dimethyl aminomethyl) phenol, the vulcanization of the resulting polymer was carried out and the physical properties of the vulcanized product were tested. The results are shown in Table 1.
  • a copolymer of tetrafluoroethylene, propylene and chloroethyl vinyl ether(CEVE) (CEVE is used for crosslinkage) which had molar ratio of 54:44:2 of 4F component, P component and CEVE component and an average number molecular weight of 76,000, was vulcanized under the following condition.
  • the physical properties of the vulcanized product are shown in Table 1.
  • Foaming of the polymer in the vulcanization was found and the surface of the vulcanized product was not smooth.
  • Example 2 A vulcanization of the composition of Example 2 was carried out by an oscillating disc sheometer at 150° C. The vulcanization curve is shown in FIG. 1 together with the result of Reference.**
  • Example 2 The composition of Example 1 was kept at room temperature for 7 days or 14 days. The physical properties of the resulting vulcanized products were tested. The results are shown in Table 2.
  • Example 2 The composition of Example 2 was also kept at the room temperature for 7 days and the physical properties of the resulting vulcanized product were tested. The result is shown in Table 2.
  • the chemical resistance was tested by dipping the product in the chemical liquid under specific conditions and measuring volumetric expansion coefficient. The results are shown in Table 3.
  • the vulcanized products were prepared as follows.
  • the terpolymer having 1.1 mole of glycidyl vinyl ether component obtained in Example 2 was admixed with various vulcanizing agents and the vulcanizing conditions were tested by the oscillating disc rheometer. The results are shown in Table 4.

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Abstract

A fluoroelastomer is produced by copolymerizing propylene, tetrafluoroethylene and glycidyl vinyl ether in the presence of a polymerization initiator.

Description

BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to a process for producing a fluoroelastomer, more particularly, it relates to a process for producing a novel fluoroelastomer of propylene-tetrafluoroethylene-glycidyl vinyl ether terpolymer.
2. Description of Prior Art
It has been known that propylene-tetrafluoroethylene copolymers are excellent fluoroelastomers. (Japanese Patent Publication No. 24199/1968; U.S. Pat. No. 3,467,635 and B. Pat. No. 1,284,247)
Thus, the fluoroelastomers of propylene-tetrafluoroethylene copolymer, have excellent heat resistance and chemical resistance whereas they have inferior vulcanization properties.
In order to improve the vulcanization properties, it has been proposed to incorporate a comonomer into the copolymer for forming crosslinkable parts such as chloroethyl vinyl ether, acrylic acid, tertiary butyl acrylate, and divinyl ether.
According to the study made by the inventors, it has been found that there remain some disadvantages in the vulcanization step of the above-mentioned known ternary systems, such as blistering, insufficient vulcanization rate and necessity of high vulcanization temperature, and that most of their resultant vulcanizates show inferior heat stability to those of the binary systems.
SUMMARY OF THE INVENTION
It is an object of the present invention to provide a process for producing a propylene-tetrafluoroethylene type terpolymer which has improved vulcanization properties.
It is another object of the present invention to improve the vulcanization properties of a propylene-tetrafluoroethylene type terpolymer without a deterioration of the heat resistance and the chemical resistance.
The foregoing and other objects of the present invention have been attained by providing a process for producing a fluoroelastomer by copolymerizing propylene, tetrafluoroethylene and glycidyl vinyl ether in the presence of a polymerization initiator to obtain a propylene-tetrafluoroethylene-glycidyl vinyl ether terpolymer.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
In accordance with the present invention, a novel fluoroelastomer which is vulcanizable and comprises 50 to 65 mole % of tetrafluoroethylene component, 35 to 50 mole % of propylene component and 0.01 to 10 mole % of glycidyl vinyl ether component was obtained. It is especially preferable to produce a fluoroelastomer comprising 53 to 60 mole % of tetrafluoroethylene component, 40 to 47 mole % of propylene component, and 0.2 to 5 mole % of glycidyl vinyl ether component. When the content of the glycidyl vinyl ether is too small, the improvement of the vulcanization properties is not enough whereas when it is too much, the heat resistance in aging is deteriorated and the cost of the raw materials is disadvantageously high.
The contents of tetrafluoroethylene and propylene are preferably selected from the above-mentioned range from the viewpoints of heat resistance, chemical resistance and easy availability.
The terpolymerization of the present invention can be a bulk polymerization, a suspension polymerization, an emulsion polymerization, and a solution polymerization. A conventional catalytic polymerization, a modified redox polymerization, and a high energy ionizing radiation polymerization can be adopted.
In the terpolymerization of tetrafluoroethylene, propylene and glycidyl vinyl ether, it is possible to add suitable other monomer such as ethylene, isobutylene, vinyl fluoride, vinylidene fluoride, hexafluoropropylene, fluorovinyl ether, alkyl vinyl ether, chlorotrifluoroethylene etc. The content of the other monomer component is usually less than 15 mole %. The molecular weight of the fluoroelastomer is preferably more than about 30,000 from the viewpoint of characteristics of the vulcanized product such as tensile strength. The molecular weight of the copolymer should not be too high from the viewpoints of both of the processability and the characteristics of the vulcanized product. It is optimum to produce the fluoroelastomer having a molecular weight of about 50,000 to 150,000.
The process of the present invention is carried out under various polymerization systems and polymerization conditions. It is possible to carry out the copolymerization in an organic solvent such as fluoro- or fluorochloro-saturated hydrocarbons e.g. trichloromonofluoromethane, trichlorotrifluoroethane and perfluorocyclobutane (Freon® type solvents) and alcohols e.g. tertiary butanol. When the organic solvent is used, the copolymerization can be carried out at -40° C. to +150° C. under relatively low reaction pressure such as about 1 to 50 Kg/cm2.
It is also possible to carry out the copolymerization in an aqueous medium by a suspension polymerization or an emulsion polymerization. In the emulsion polymerization, a perfluoroalkyl or perfluorochloroalkyl type dispersing agent is preferably used.
In the suspension polymerization and the emulsion polymerization, it is possible to use a dispersion stabilizer such as chlorinated hydrocarbons, liquid hydrocarbons, trichlorotrifluoroethane and tertiary butanol, a reaction accelerator and other additives.
Polymerization initiators such as peroxides, azo compounds and persulfates can be used. The copolymerization can be also carried out by a high energy ionizing radiation such as γ-ray resulted by cobalt-60.
In the copolymerization in an aqueous medium, it is possible to carry it out at about 50° to 100° C. under a pressure of about 5 to 200 Kg/cm2. When a redox catalyst is used as a polymerization initiator, the copolymerization can be carried out at lower temperature such as -20° C. to +50° C.
The process of the present invention can be carried out by a batch system, a semi-continuous system or a continuous system. The polymerization conditions, polymerization operation and polymerization apparatus can be preferably selected depending upon the purpose and the polymerization system.
Thus, a transparent or white fluoroelastomer having rubber-like elasticity can be obtained. The fluoroelastomer having superior vulcanizability than that of the conventional propylene-tetrafluoroethylene copolymer (elastomer) can be obtained.
The resulting fluoroelastomer can be treated by various crosslinking agents such as organic peroxides and amines to crosslink it whereby a rubber like crosslinked product is obtained. It is possible to crosslink by high energy ionizing radiation such as γ-rays or electron rays. In this case, it is possible to add various crosslinking adjuvants, fillers and reinforcing agents to give various compositions for vulcanization.
The novel fluoroelastomers of the present invention an be vulcanized in various formulations under various conditions. It is especially characteristic to be vulcanizable at low temperature such as room temperature by selecting a specific formulation. Thus, the fluoroelastomers of the present invention can be also utilized as the room temperature vulcanizable elastomer.
When one of tertiary amines e.g. monoamines, polyamines or salts thereof or a mixture of the tertiary amine and a hydroxyl compound having at least one --OH group, is used as a vulcanizing agent, it is possible to vulcanize the elastomer at room temperature whereby the vulcanizing velocity is sufficiently high and vulcanized products having excellent heat stability can be obtained.
Suitable tertiary amines include benzyl dimethyl amine, α-methylbenzyl dimethyl amine, dimethyl aminomethyl phenol, tris (dimethyl aminomethyl) phenol, diethylaminopropyl amine, N-aminoethyl piperadine, ethyl methyl imidazole, triethylene diamine, N,N'-bis(alkyl) piperadine, 4,4'-trimethylenedipyridine, 2,3-bis(2-pyridyl)-5,6-dihydropyradine, N-ethyl morphorine, 1,8-diaza bicyclo(5,4,0) undecene-7 and salts thereof.
Suitable hydroxyl compounds used with the tertiary amine include octanol, cyclohexanol, phenol, ethyleneglycol, propyleneglycol, polyethyleneglycol, polypropyleneglycol, hydroquinone, catechol, resorcinol, 2,2'-bis(4-hydroxyphenyl) propane[bisphenol A], 1,3,5-trihydroxybenzene, dihydroxynaphthalene, 4,4'-dihydroxydiphenyl, 4,4'-dihydroxystilbene, 2,2'-bis(4-hydroxyphenyl) butane [bisphenol B], 2,4-dihydroxybenzophenone, 2,4-dihydroxybenzoate, 4,4'-dihydroxydiphenylsulfone, 2-methyl resorcinol, trimethylol allyloxyphenol and tris(4-hydroxyphenyl) methane.
Other vulcanizing agents such as aromatic polyamines can be also used though chemical stability of crosslinkage is slightly inferior.
Suitable aromatic polyamines include xylene diamine, methaphenylene diamine, diamino-diphenyl methane and diaminodiphenyl sulfone.
It is also possible to use alicyclic or heterocyclic polyamines such as menthane diamine and bisaminopropyl tetraoxa-spiroundecene.
The typical formulations for vulcanization at room temperature are as follows.
______________________________________                                    
Fluoroelastomer      100 wt. parts                                        
M T-carbon black     5 to 60 wt. parts                                    
Hydroquinone         0.2 to 2 wt. parts                                   
Tris(dimethylaminomethyl)                                                 
                     0.2 to 2 wt. parts                                   
phenol                                                                    
______________________________________
These components are blended on a mixing roll mill and the blended composition is kept at room temperature for 3 to 14 days to obtain a vulcanized elastomer having enough strength such as tensile strength of higher than 100 Kg/cm2. It is possible to improve the heat resistance by incorporating a metal oxide or silica.
It is also possible to prepare a solution paint by dissolving the composition in a suitable solvent. A vulcanized rubber coat having high strength can be obtained by coating the solution paint and maintaining it for 3 to 14 days after the coating.
Suitable solvents include ethyl acetate, tetrahydrofuran, and 1,1,2-trichlorotrifluoroethane.
Various additives used in the conventional crosslinking processes can be also added in the crosslinking process of the fluoroelastomer of the present invention. These additives include metal oxides such as magnesium oxide and lead oxide; reinforcing agents such as carbon black and fine silica; other fillers; pigments; antioxidants and stabilizers.
When the additive is added to the fluoroelastomer, it is preferable to uniformly mix it with the fluoroelastomer.
The mixing operation is usually carried out by using the conventional rubber blending roll mill and Bumbary mixer, the condition for the mixing operation is not critical. The additives can be thoroughly dispersed in the fluoroelastomer. It is preferable to select the optimum condition and operation in the mixing operation depending upon the kinds of the raw materials and the ratios thereof and the purposes.
The fluoroelastomer obtained by the process of the present invention can be vulcanized at the conventional high temperature of 100° to 250° C. as well as at room temperature. The above-mentioned vulcanizing agents and adjuvants can be used.
The heat crosslinking process using the chemical crosslinking agent can be the conventional process. For example, the mixture is heated in a mold by means of a conventional press, transfer and injection molding, or the mixture is fabricated by the extrusion process followed by heating in an air or steam oven or other device. It is preferable to select the optimum condition in the heat crosslinking process depending upon the kinds of the raw materials and the ratios thereof. The temperature in the crosslinking process is usually in a range of about 80° to 250° C. preferably about 120° to 200° C. The time for heating is not critical and it is usually in a range of 1 minute to 2 hours preferably 3 minutes to 2 hours depending upon the kind of the chemical crosslinking agent. When the temperature is high, the time for heating can be short. The crosslinked copolymer can be post cured improve its physical properties. For example, the post cure treatment is carried out at 150° to 250° C. preferably 180° to 230° C. for about 15 to 25 hours.
The crosslinked fluoroelastomers produced by the process of the present invention have high heat resistance and chemical resistance as well as high solvent resistance except for certain solvents of such as lower alkane, ketones and esters. Accordingly, the crosslinked fluoroelastomers can be effectively used for various usages requiring elasticity in various conditions for the uses, for example, O-ring for cars, gaskets, valve-stem seals, diaphragms, sealings for dry-cleaning apparatus, pipe, flexible joints, hoses for chemical industrial uses, rolls, packings and grooves. The crosslinked fluoroelastomers are especially useful as the materials which contact with an oil, a solvent or a corrosive liquid. The crosslinked fluoroelastomers can be molded in a form of pipe or rod and they can be also processed as a primary step to form a film or a tape which is further processed by a lamination, a coating and a wind-wrapping as the secondary step.
The following examples are intended merely to describe specific embodiments of the present invention and are not to be construded as a limitation on the scope of the invention.
EXAMPLE 1
In a 1 liter autoclave equipped with a stirrer, 375 g of water (oxygen is removed), 60 g of tertiary butanol, 2.9 g of ammonium perfluorooctanate, 1.5 g of ammonium persulfate, 0.4 g of sodium thiosulfate and 0.3 g of ferrous sulfate were charged and then 0.15 g of sodium hydroxide was added to adjust pH to 9.5. The autoclave was purged with nitrogen, 0.9 g (0.009 mole) of glycidyl vinyl ether(GVE) 5.6 g (0.13 mole) of propylene (P) and 80 g (0.8 mole) of tetrafluoroethylene (4F) were charged under spontaneous pressure.
The mixture was stirred at 300 rpm and the temperature in the autoclave was raised to 35° C. When the reaction was initiated to decrease the pressure, the monomer mixed gas of 4F, P and GVG of molar ratios of 53:45:2 was charged to maintain the pressure of 26 Kg/cm2 for 8 hours. After the reaction, the remained monomers were purged and the resulting latex was discharged and 1% aqueous solution of CaCl2 added to coagulate and the product was washed and dried to obtain 81.0 g of a polymer.
The resulting polymer had molar ratios of 54.1:43.8:2.1 of tetrafluoroethylene(4F) component, propylene(P) component and glycidyl vinyl ether(GVE) component (NMR analysis), and had about 30% hydrated glycidyl groups (IR analysis).
The copolymer had an average number molecular weight of 75,000 and mooney viscosity (ML1+4) at 100° C. of 68 and a Shore A hardness of 45.
A vulcanization was carried out by admixing 100 wt.parts of a copolymer with 1 wt.part of hydroquinone, 0.5 wt.part of tris(dimethylaminomethyl) phenol, 25 wt.parts of MT carbon and 10 wt.parts of lead oxide and press-vulcanizing the mixture at 150° C. under the pressure of 100 Kg/cm2 for 20 minutes. The product was taken out from the mold and was heated at 200° C. for 22 hours in an oven to vulcanize it. The main mechanical properties of the vulcanized product and the test result of heat aging test are shown in Table 1.
EXAMPLE 2
In accordance with the process of Example 1 except charging 0.45 g(0.0045 mole) of glycidyl vinyl ether at the initiation and charging the monomer mixed gas of 4F, P and GVE of molar ratios of 51:45:1, during the reaction. The copolymerization was carried out for 6 hours to obtain 69.8 g of the polymer having molar ratios of 53.1:45.8:1.1 of 4F component, P component and GVE component and an average number molecular weight of 69,000, and mooney viscosity (ML1+4) at 100° C. of 77.
In accordance with the process of Example 1, the vulcanization of the resulting polymer was carried out and the physical properties of the vulcanized product were tested. The results are shown in Table 1.
EXAMPLE 3
In accordance with the process of Example 1 except using 2 wt.parts of diaminodiphenyl methane instead of hydroquinone and tris(dimethyl aminomethyl) phenol, the vulcanization of the resulting polymer was carried out and the physical properties of the vulcanized product were tested. The results are shown in Table 1.
              Table 1                                                     
______________________________________                                    
             Example 1                                                    
                   Aging                                                  
             No    260° C.      Refer-                             
             aging 5 days  Ex.2   Ex.3 ence*                              
______________________________________                                    
Tensile strength                                                          
(Kg/cm.sup.2)  235     205     178  203  137                              
Elongation (%) 198     150     260  230  218                              
100% modulus (Kg/cm.sup.2)                                                
               82      140     48   66   38                               
Hardness (Shore A)                                                        
               77       78     72   75   73                               
Compression                                                               
permanent strain (%)                                                      
               49      --      31   24   66                               
200° C. . 22 hours                                                 
______________________________________                                    
 *Reference
A copolymer of tetrafluoroethylene, propylene and chloroethyl vinyl ether(CEVE) (CEVE is used for crosslinkage) which had molar ratio of 54:44:2 of 4F component, P component and CEVE component and an average number molecular weight of 76,000, was vulcanized under the following condition. The physical properties of the vulcanized product are shown in Table 1.
Foaming of the polymer in the vulcanization was found and the surface of the vulcanized product was not smooth.
______________________________________                                    
Composition                                                               
______________________________________                                    
Fluoroelastomer      100 wt. parts                                        
MT-carbon             20 wt. parts                                        
MgO                   15 wt. parts                                        
Tetraethylene pentaamine                                                  
                      2 wt. parts                                         
Vulcanization                                                             
Press vulcanization  180° C. . 30 min.                             
Oven vulcanization   204° C. . 20 hours                            
______________________________________
EXAMPLE 4
A vulcanization of the composition of Example 2 was carried out by an oscillating disc sheometer at 150° C. The vulcanization curve is shown in FIG. 1 together with the result of Reference.**
From the vulcanization curves, the superiority of effect of glycidyl vinyl ether as crosslinkage to that of of the conventional one is clearly found.
______________________________________                                    
** Reference                                                              
Copolymer of 4F, P and CEVE                                               
(molar ratio of 54:44:2)                                                  
Average number                                                            
molecular weight       76,000                                             
Composition                                                               
Fluoroelastomer        100 wt. parts                                      
MT carbon               20 wt. parts                                      
MgO                     15 wt. parts                                      
Tetraethylene pentaamine                                                  
                        2 wt.parts                                        
______________________________________
EXAMPLE 5
The composition of Example 1 was kept at room temperature for 7 days or 14 days. The physical properties of the resulting vulcanized products were tested. The results are shown in Table 2.
EXAMPLE 6
The composition of Example 2 was also kept at the room temperature for 7 days and the physical properties of the resulting vulcanized product were tested. The result is shown in Table 2.
It was found that the vulcanization at room temperature could be easily performed by introducing the glycidyl group having high reactivity in the polymer though it was not attained by the conventional crosslinking parts.
              Table 2                                                     
______________________________________                                    
           Example 5                                                      
           150° C. . 20min.                                        
                     R.T.    R.T.    Exp.6                                
           200° C. . 22hr.                                         
                     7 days  14 days 7 days                               
______________________________________                                    
Tensile strength                                                          
             235         141     165   108                                
(Kg/cm.sup.2)                                                             
Elongation (%)                                                            
             198         253     220   360                                
100% modulus 82          47      53    40                                 
(Kg/cm.sup.2)                                                             
Hardness (Shore A)                                                        
             77          75      76    73                                 
______________________________________
EXAMPLE 7
The chemical resistances of the vulcanized fluoroelastomers obtained in Examples 2 and 3 and the vulcanized fluoroelastomer obtained in Reference which had crosslinking part of CEVE. The chemical resistance was tested by dipping the product in the chemical liquid under specific conditions and measuring volumetric expansion coefficient. The results are shown in Table 3. The vulcanized products were prepared as follows.
______________________________________                                    
               Ex.4-A                                                     
                      Ex.4-B Ref. A  Ref. B                               
______________________________________                                    
Polymer:                                                                  
4F/P/GVE                                                                  
 (molar ratio 53.1 : 45.8 : 1.1)                                          
                 100     --      --    --                                 
 (MW 69,000)                                                              
 4F/P/GVE                                                                 
 (molar ratio 54.1 : 43.8 : 2.1)                                          
                 --      100     --    --                                 
 (MW 75,000)                                                              
 4F/P/CEVE                                                                
 (molar ratio 54 : 44 : 2)                                                
                 --      --      100   --                                 
 (MN 76,000)                                                              
 4F/P                                                                     
 (molar ratio 55 : 45                                                     
                 --      --      --    100                                
 (MW 180,000)                                                             
Vulcanizer:                                                               
 hydroquinone    1       --      --    --                                 
 tris(dimethylaminomethyl)                                                
                 0.5     --      --    --                                 
 phenol                                                                   
 diaminodiphenyl methane                                                  
                 --      2       --    --                                 
 tetraethylenepentamine                                                   
                 --      --      2     --                                 
 α,α'-bis(t-butylperoxy)-                                     
                 --      --      --    2                                  
 p-diisopropyl benzene                                                    
 tri-allyl isocyanurate                                                   
                 --      --      --    --                                 
 MT carbon       25      25      20    25                                 
 MgO             --      --      15    --                                 
 PbO             10      10      --    10                                 
Vulcanization:                                                            
 Press vulcanization                                                      
                 150° C.                                           
                         150° C.                                   
                                 180° C.                           
                                       150° C.                     
                 20 min  20 min  30 min                                   
                                       40 min                             
 Oven vulcanization                                                       
                 200° C.                                           
                         200° C.                                   
                                 204° C.                           
                                       200° C.                     
                 22 hr   22 hr   20 hr 20 hr                              
______________________________________                                    

                                  Table 3                                 
__________________________________________________________________________
        Dipping        Ref. A Ref. B                                      
Chemical                                                                  
        Condition                                                         
             Exp. 4-A                                                     
                  Exp. 4-B                                                
                       4F/P/CEVE                                          
                              4F/P                                        
liquid  ° C. days                                                  
             4F/P/GVE  copolymer                                          
                              copolymer                                   
__________________________________________________________________________
H.sub.2 SO.sub.4 (96%)                                                    
        100° C.                                                    
             5.3  4.1  12     4.4                                         
        3 day                                                             
HNO.sub.3 (60%)                                                           
        "    27   107  ***    34                                          
NaOH (50%)                                                                
        "    -0.2 -0.3 30     1.1                                         
ASTM #3 oil                                                               
        175° C.                                                    
             11   9    13     15                                          
        3 days                                                            
Fuel oil 13                                                               
        R.T. 55   50   56     58                                          
        7 days                                                            
__________________________________________________________________________
 *** decomposed
EXAMPLE 8
The terpolymer having 1.1 mole of glycidyl vinyl ether component obtained in Example 2 was admixed with various vulcanizing agents and the vulcanizing conditions were tested by the oscillating disc rheometer. The results are shown in Table 4.
                                  Table 4                                 
__________________________________________________________________________
         1   2   3   4   5   6   7   8   9                                
__________________________________________________________________________
Fluoroelastomer                                                           
         100 100 100 100 100 100 100 100 100                              
MT carbon                                                                 
         35  35  35  35  35  35  35  35  35                               
MgO                                      10                               
Triethylenedi-                                                            
amine    2                                                                
Benzyl dimethyl                                                           
amine        1                                                            
Tris(dimethyl                                                             
aminomethyl)     1   1   1   0.5                                          
phenol                                                                    
Diazabicyclo                                                              
undecene                         0.5                                      
Ethylene-                                                                 
glycol           1                                                        
Phenol               1                                                    
Hydroquinone 1           1   1   1                                        
Diaminodiphenyl                                                           
methane                              2   2                                
    T.sub.10                                                              
         1.7 3.1 1.4 1.0 0.9 1.5 0.8 0.5 1.8                              
ODR T.sub.90                                                              
         14.5                                                             
             24.2                                                         
                 13.4                                                     
                     9.7 12.5                                             
                             13.0                                         
                                 10.7                                     
                                     9.5 16.6                             
Test                                                                      
    T.sub.Δ80                                                       
         12.8                                                             
             21.1                                                         
                 12.0                                                     
                     8.7 11.6                                             
                             11.5                                         
                                 9.9 8.6 14.8                             
result                                                                    
    TR min.                                                               
         9.0 14  13  13  19  13  18  39  42                               
150° C.                                                            
    TR max.                                                               
         77  33  83  84  114 86  101 122 128                              
    ΔTR                                                             
         68  19  70  71  95  73  83  83  86                               
__________________________________________________________________________

Claims (2)

What is claimed is:
1. An uncured fluoroelastomer carbo-polymerized copolymer of composition 50 to 65 mole % tetrafluoroethylene, 35 to 50 mole % propylene and 0.01 to 10 mole % glycidylvinyl ether monomer wherein said fluoroelastomer copolymer contains side chains with unreacted glycidyl groups which are derived from said glycidylvinyl ether monomer.
2. The fluoroelastomer copolymer of claim 1 wherein the amount of glycidyl vinyl ether component is 0.2 to 5 mole %.
US05/860,198 1976-12-16 1977-12-13 Process for producing fluoroelastomer and crosslinked polymer thereof Expired - Lifetime US4151342A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4316941A (en) * 1979-10-02 1982-02-23 Asahi Glass Company Ltd. Rubber stopper for sealing
US4321306A (en) * 1978-11-17 1982-03-23 Tsukasa Eguchi Rubber stopper for tight sealing
US4732734A (en) * 1985-07-15 1988-03-22 Kernforschungszentrum Karlsruhe Gmbh Method for preventing fluoroelastomer-related hydrolysis of fluorine-containing gas streams in contact with fluoroelastomeric articles of an industrial gas stream handling system
US5349031A (en) * 1992-04-24 1994-09-20 Asahi Glass Company Ltd. Fluorine-containing coating composition
US5508355A (en) * 1992-04-03 1996-04-16 E. I. Du Pont De Nemours And Company Vulcanizable fluorine-containing elastomer composition
US6559238B1 (en) * 1998-06-29 2003-05-06 E. I. Du Pont De Nemours And Company Thermally cross-linked fluoropolymer
US20070276097A1 (en) * 2006-05-26 2007-11-29 Asahi Glass Company, Limited Cross-linkable fluoroelastomer, its composition and cross-linked rubber molded product
US20100036073A1 (en) * 2008-08-08 2010-02-11 E. I. Du Pont De Nemours And Company Non-Melt-Flowable Perfluoropolymer Comprising Repeating Units Arising From Tetrafluoroethylene and a Monomer Having a Functional Group and a Polymerizable Carbon-Carbon Double Bond
US20140363679A1 (en) * 2012-01-17 2014-12-11 Nichias Corporation Material for gasket
EP3722340A4 (en) * 2017-12-06 2021-05-12 AGC Inc. ELASTIC COPOLYMER CONTAINING FLUORINE AND PROCESS FOR PRODUCING AN ELASTIC COPOLYMER CONTAINING FLUORINE

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US2839514A (en) * 1950-05-23 1958-06-17 Shell Dev Copolymer of allyl glycidyl monoether and styrene
US3431245A (en) * 1963-09-20 1969-03-04 Polymer Corp Production of novel polymers and polymerization process therefor
US3467635A (en) * 1964-10-30 1969-09-16 Du Pont Copolymers of tetrafluoroethylene and olefins curable to elastomers
US3697218A (en) * 1969-08-27 1972-10-10 American Cyanamid Co Flame-proof fibers
US3718558A (en) * 1969-12-11 1973-02-27 Asahi Glass Co Ltd Process for producing a cross-linked copolymer of tetrafluoroethylene and propylene using high energy ionizing radiation
US3825510A (en) * 1970-12-30 1974-07-23 Asahi Glass Co Ltd Method for cross-linking copolymers of tetrafluoroethylene and propylene
US3892641A (en) * 1970-05-26 1975-07-01 Japan Atomic Energy Res Inst Process for producing a copolymer of tetrafluoroethylene and propylene
US3933773A (en) * 1972-06-08 1976-01-20 Thiokol Corporation Thermoplastic elastomeric copolymers and terpolymers of tetrafluoroethylene and propylene and method of making the same

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US2839514A (en) * 1950-05-23 1958-06-17 Shell Dev Copolymer of allyl glycidyl monoether and styrene
US3431245A (en) * 1963-09-20 1969-03-04 Polymer Corp Production of novel polymers and polymerization process therefor
US3467635A (en) * 1964-10-30 1969-09-16 Du Pont Copolymers of tetrafluoroethylene and olefins curable to elastomers
US3697218A (en) * 1969-08-27 1972-10-10 American Cyanamid Co Flame-proof fibers
US3718558A (en) * 1969-12-11 1973-02-27 Asahi Glass Co Ltd Process for producing a cross-linked copolymer of tetrafluoroethylene and propylene using high energy ionizing radiation
US3892641A (en) * 1970-05-26 1975-07-01 Japan Atomic Energy Res Inst Process for producing a copolymer of tetrafluoroethylene and propylene
US3825510A (en) * 1970-12-30 1974-07-23 Asahi Glass Co Ltd Method for cross-linking copolymers of tetrafluoroethylene and propylene
US3933773A (en) * 1972-06-08 1976-01-20 Thiokol Corporation Thermoplastic elastomeric copolymers and terpolymers of tetrafluoroethylene and propylene and method of making the same

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4321306A (en) * 1978-11-17 1982-03-23 Tsukasa Eguchi Rubber stopper for tight sealing
US4316941A (en) * 1979-10-02 1982-02-23 Asahi Glass Company Ltd. Rubber stopper for sealing
US4732734A (en) * 1985-07-15 1988-03-22 Kernforschungszentrum Karlsruhe Gmbh Method for preventing fluoroelastomer-related hydrolysis of fluorine-containing gas streams in contact with fluoroelastomeric articles of an industrial gas stream handling system
US5508355A (en) * 1992-04-03 1996-04-16 E. I. Du Pont De Nemours And Company Vulcanizable fluorine-containing elastomer composition
US5349031A (en) * 1992-04-24 1994-09-20 Asahi Glass Company Ltd. Fluorine-containing coating composition
US6559238B1 (en) * 1998-06-29 2003-05-06 E. I. Du Pont De Nemours And Company Thermally cross-linked fluoropolymer
US20070276097A1 (en) * 2006-05-26 2007-11-29 Asahi Glass Company, Limited Cross-linkable fluoroelastomer, its composition and cross-linked rubber molded product
US8044145B2 (en) * 2006-05-26 2011-10-25 Asahi Glass Company, Limited Cross-linkable fluoroelastomer, its composition and cross-linked rubber molded product
US20100036073A1 (en) * 2008-08-08 2010-02-11 E. I. Du Pont De Nemours And Company Non-Melt-Flowable Perfluoropolymer Comprising Repeating Units Arising From Tetrafluoroethylene and a Monomer Having a Functional Group and a Polymerizable Carbon-Carbon Double Bond
US20140363679A1 (en) * 2012-01-17 2014-12-11 Nichias Corporation Material for gasket
KR20150009947A (en) * 2012-01-17 2015-01-27 니찌아스 카부시키카이샤 Material for gasket
US9638325B2 (en) * 2012-01-17 2017-05-02 Nichias Corporation Material for gasket
EP3722340A4 (en) * 2017-12-06 2021-05-12 AGC Inc. ELASTIC COPOLYMER CONTAINING FLUORINE AND PROCESS FOR PRODUCING AN ELASTIC COPOLYMER CONTAINING FLUORINE
US11306167B2 (en) 2017-12-06 2022-04-19 AGC Inc. Fluorinated elastic copolymer, and method for producing fluorinated elastic copolymer

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